Hydrogen permeation in PEM electrolyzer cells operated at asymmetric pressure conditions

verfasst von
P. Trinke, B. Bensmann, S. Reichstein, R. Hanke-Rauschenbach, K. Sundmacher
Abstract

The present contribution investigates the hydrogen permeation through a fumea EF-40 catalyst coated membrane during PEM water electrolysis. The permeation is characterized at different temperatures and different pressure gradients across the membrane. The measured permeation fluxes show a quadratic dependence on the pressure difference. A permeation model combining a diffusive and convective transport can describe the experimental data quantitatively. The determined diffusive permeability coefficient KP,diffeff = 2.95 × 10-14 mol/(m s Pa)at 60 °C and its temperature dependence agrees very well with literature values. A convective permeability coefficient of the membrane is proposed for the description of the quadratic dependence. The obtained convective permeability coefficient KP,conveff = 9.02 × 10-21 mol/(m s Pa2)at 60 °C indicates a high hydraulic permeability in comparison with recently reported values. This high hydraulic permeability can be attributed especially to the low equivalent weight of the investigated membrane. Additionally, the operating conditions are suspected to support permeation.

Organisationseinheit(en)
Fachgebiet Elektrische Energiespeichersysteme
Externe Organisation(en)
Otto-von-Guericke-Universität Magdeburg
Max-Planck-Institut für Dynamik komplexer technischer Systeme
Typ
Artikel
Journal
Journal of the Electrochemical Society
Band
163
Seiten
F3164-F3170
ISSN
0013-4651
Publikationsdatum
24.08.2016
Publikationsstatus
Veröffentlicht
Peer-reviewed
Ja
ASJC Scopus Sachgebiete
Elektronische, optische und magnetische Materialien, Erneuerbare Energien, Nachhaltigkeit und Umwelt, Oberflächen, Beschichtungen und Folien, Elektrochemie, Werkstoffchemie
Ziele für nachhaltige Entwicklung
SDG 7 – Erschwingliche und saubere Energie
Elektronische Version(en)
https://doi.org/10.1149/2.0221611jes (Zugang: Geschlossen)